EP1363098B1

EP1363098B1 - Tempering apparatus

Info

Publication number: EP1363098B1
Application number: EP02076586A
Authority: EP
Inventors: Anders Conradsen Kongstad
Original assignee: Aasted Mikroverk ApS
Current assignee: Aasted Mikroverk ApS
Priority date: 2002-04-22
Filing date: 2002-04-22
Publication date: 2004-02-04
Anticipated expiration: 2022-04-22
Also published as: EP1363098A1; US6960014B2; DE60200203T2; DK1363098T3; ATE259051T1; US20040081017A1; ES2213135T3; TR200400882T4; DE60200203D1

Abstract

Tempering apparatus having disc-free stirring tool (8) with plate-shaped arms (12, 13). The upper side (14) of each arm (12) has a different geometrical configuration than the lower side (19) thereof. Each neighbouring arm (13) has the opposite configuration of the upper and lower sides (23 and 24). The mass is thereby given an intermittent up- and downwards movement in the mass treatment chamber (2) and the tempering capacity of the apparatus is improved. <IMAGE>

Description

The present invention concerns the technical field of apparatuses for continuous tempering of fat-containing mass, for example chocolate-like mass or chocolate mass comprising cocoa butter.

An apparatuses known from WO-A- 92/000 15 comprises at least one mass treatment chamber comprising a stirring tool arranged therein, which is being driven by a central shaft, and which stirring tool is free from a disc, as it only comprises mixing arms, which are radially extending, and are plate shaped having mixing obstacles.

By the tempering process the mass is brought to around 40-50°C, whereafter it is being cooled to around 25-34°C so that crystallisation is initiated. Then the mass is reheated around 0,5-2,0°C for re-melting most of the in-stable crystals in the mass, however preserving a content of stable β-crystals which melts at a higher temperature than the in-stable crystals. The stable crystals are preserved in the mass ready for depositing in an amount of typically 0,01 % - 5%, preferably in an amount of 0,1% - 2%.

Generally, fat-containing masses are suspensions of non-fat particles such as sugar, milk powders and cocoa solids mixed up with a liquid fat constituent. When it comes to chocolate mass, the fat phase comprises genuine cocoa butter of until around 30%, but may comprise substitutes as well when we are talking about chocolate-like masses. Such substitutes can be in the form of other types of fat-containing oils. Chocolate types where the cocoa butter has been replaced wholly or partly by other fats are often named commercially as compound chocolate, in which the cocoa butter has been replaced by palm-kernel oil. Mass made of 100% fat in the form of cocoa butter or the like as compound is also possible.

However, for the tempering to be performed, it is decisive, that whether the fat phase constitutes of genuine cocoa butter or substitutes therefore, that the fat phase is capable of crystallizing into stable crystal types, such as the β-crystals developing in genuine cocoa butter when the mass solidifies.

The chocolate-like mass is brought to a tempered, liquid state and then deposited in moulds, on top of the pre-made articles or for covering the upper open surfaces of the articles.

An apparatus of the introductory kind for tempering chocolate mass was invented by Aasted in 1945. The apparatus has a plurality of mass treatment chambers arranged in a column with intermediary water chambers connected to a circuit, in which the temperature of the water could be regulated before entering the water chambers. The stirring tools comprised two plate shaped arms having the same identical configuration of the upper and lower sides of the blades. All the mixing blades had the same shape and configuration and was arranged in identical patterns on both sides of the arms.

EP 0 289 849 A2 (SOLLICH) discloses another apparatus of the above kind by which the stirring tool comprises four plate-shaped arms arranged in a cross. The geometrical configurations on each side of the arms were identical. The width of the arms were the same at the centre where the arms are connected to the shaft, as at the ends of the arms at the periphery of the mass treatment chamber. Tests revealed, that the arms had a very high drag coefficient in the mass and to a severe extent dragged the mass around in the chamber in comparison with a stirring tool having only two arms. The mixing of the mass is only performed in two dimensions, i.e. over the planar heat-exchange surface of the chamber.

EP 0806149 A2 (AASTED) describes a further tempering apparatus of the introductory type, by which the stirring tool comprises two arms having identical geometrical configurations on each sides. The drag in the mass is reduced severely as the arms are tapered towards the ends. The much higher velocity of the ends of the arms in comparison with the velocity at the centre is thereby taken into account or balanced with a view of severely reducing the drag resistance in the mass. The arms are provided with openings at the centre for providing axial flow at the centre zone, however the mixing of the mass at the far major remaining part of the mass chamber is performed in two dimensions only.

WO 92 00015 A (AASTED-MIKROVERK APS) discloses an apparatus for continuous tempering of chocolate mass comprising a plurality of mass chambers in each of which is arranged a stirring tool driven by a central axis. Each stirring tool has the form of two oppositely and radially extending plate-shaped arms (fig. 2 and 3). The upper and lower sides of the arms are identical in their geometrical configurations. The lower sides of the arms disclosed in figure 3 have identical geometrical configurations. The upper sides of the arms disclosed in figure 3 have scrapers arranged at different geometrical positions, which provides for horizontal mixing movements of the mass.

EP 1 175 837 A (AASTED-MIKROVERK APS) discloses an apparatus for continuous tempering of chocolate mass with a plurality of mass chambers. In each mass chamber is arranged a disc-shaped stirring tool, which divides the mass chamber into a lower part and an upper part. The mass passes from the lower part and to the upper chamber part through openings at the centre or through a peripheral gap. Each disc-shaped stirring tool is assembled by two opposite wings and an intermediary disc element. In each chamber the opposite wings are kept tight against the intermediary disc element, so that only the outer surfaces of the wings having scraper blades functions as integrated parts of the disc surfaces, which influences the chocolate. The wings are engaged in recesses in the disc element so that they are functionally a part thereof. The discs are mandatory as mixing tools and the only reason for the engaged wings embedded into the discs is, that by changing the discs the configuration of the mixing elements of the discs can be changed.

The intermediary disc-shaped stirring elements functions as a bar against up- and down movements in the mass chambers as mass movements are restricted to within the upper part of the chamber and to within the lower part of the chamber-effectively divided by the intermediary disc elements.

The prior art is silent about any hints or pointers to solutions, which could guide the skilled person in the direction of a solution which mixes the mass thoroughly by vertical movements.

GB 644,312 (ATLAS) discloses in 1950 a further apparatus for tempering of the above described type, however, the stirring tools are laid out as discs separating the mass treatment chambers in lower and upper chamber parts. The mass enters a chamber through a central ring-shaped gap extending around the shaft, and runs radially out towards the periphery in the lower chamber part. The mass passes through a ring-shaped gap between the periphery of the disc and the peripheral wall of the mass chamber and runs further on in the upper chamber part in towards an upper ring-shaped gap at the shaft through which the mass leaves the chamber and enters the next following chamber. The two sides of the discs are provided with mixing obstructions.

EP 1 004 244 A1 (SOLLICH) discloses a further chocolate tempering apparatus like the one described in the above referred GB 644,312, the only difference seems to be details such as the design of the mixing obstacles. However, the mixing of the mass only gives movements in two dimensions, i.e. in the planar extension of the slim mixing chamber gap between the surfaces of the mixing disc and the adjacent upper or lower surface of the mass chamber. The apparatus having disc shaped mixing tools are impossible to drain out completely from chocolate mass when required, for example when another chocolate type is to be tempered through the apparatus, i.e. when dark chocolate is to be drained out before white chocolate is to be tempered. The problem escalates when the mass to be drained out is of a high viscous type, such as nougat or crème-fillings. The mass simply covers or glues to the disc surfaces especially when they are provided with so many mixing obstacles or knobs as disclosed in the EP publication, i.e. between 24 and 36 knobs on each side of the discs.

The tempering capacity of a tempering apparatus is defined as the maximal capability in kilograms pro hour to temper a fat-containing mass having a predetermined content of for example 5% of a desired type, stable β-crystals, such as the βV-crystals. When comparising the tempering capacity of two different apparatuses it is then important, that the content of the tempered masses are as identical as possible.

The large surfaces of the mixing discs in comparison with the surfaces of mixing arms are suspected to be capable of achieving slightly higher tempering capacity when working on the same heat exchange surface area. However, concomitant disadvantages with the discs are the severe flow resistance exhibited to the mass in comparison with the arms as well as lack of possibility of high mixing intensity of the mass.

Consequently, a high flow resistance and therefore contra pressure against the mass in the apparatus having discs require a much more forceful pump to press the mass through than by the apparatus having stirring tools with arms. The high flow resistance makes it in fact impossible to completely empty the apparatus with discs from mass. Neither does the discs give any contribution to the movement of the mass through the apparatus as the stirring tools having arms does. The mass pump therefore has to be much more forceful and then expensive for an apparatus having discs than for one having stirring arms.

The other problem with the discs is the partitioning of the mass chambers in two parts which completely excludes any vertical mass flow in the mass chamber and certainly makes intermixing of mass from the one partitioning with mass in the other partitioning of the chamber impossible. Especially in the crystals creating zone or area where crystals are created with high intensity on the heat exchange surfaces, the crystals have to be removed fast and be mixed and distributed quickly and homogenously into the remaining mass in the chamber.

The objective problem to solve is to provide a tempering apparatus, which is free from discs and therefore capable of being drained empty from mass and especially from highly viscous mass, however which exhibits a high tempering capacity as well.

The apparatus according to the invention comprises the features according to claim 1.

The mass is moved vertically up and down in the chamber in an intermittent sequence. The movements works simultaneously with the mixing provided by the mixing obstacles. The intermittent sequence of the vertically directed up- and downwardly directed flow of the mass effectively distributes the cold or heat from the heat exchange surfaces into the mass.

Tests have revealed an improvement of astonishing 30-60% in tempering capacity for the inventive solution in comparison with the traditional stirring tools with plate-shaped arms - and yet may the new apparatus be completely emptied from any mass and especially from highly viscous mass. The improvement depended upon the type of mass tempered, however for traditional and widely used milk-chocolate types the average improvement was around 50%. The new stirring tool was furthermore tested in comparison with discs of the previously describes type. The tests revealed improvements in tempering capacity in comparison with the discs as well. Astonishingly, the improvements was between 10-30% in tempering capacity.

By different geometrical configuration is meant, that the shape of the one side of an arm secures a severely lower drag resistance or flow resistance through the mass, than the shape of the other side of the arm. If mixing obstacles are provided on both sides of the arms the number of obstacles at the one side of the arm shall be much lesser than at the other side. At the one side may for example be arranged two obstacles and at the other side may be arranged 4-10 obstacles. The obstacles could for example be essentially identical mixing blades at both sides of the arm or identical mixing knobs at both sides of the arm. The drag resistance may also be reduced severely if the shape or configuration of the obstacles at the one side is altered, for example by reducing the width of the obstacles drastically in comparison with the width of the obstacles at the other side of the arms. Optional is when the one side is essentially free from mixing obstacles and the other side comprises 3- 6 mixing obstacles

Decisive for obtaining different geometrical configuration of the two sides of the arms is then that a different resistance in the mass flow is achieved. A pressure difference between the two sides is then created and the mass is influenced to the intermittent up-and down movements behind the trailing edge of an arm.

In conclusion the inventive apparatus comprises a stirring tool which is free from a disc, as it only comprises mixing arms, however it achieves the same high tempering capacity.

To the contrary from the prior known disc-free tempering apparatuses the inventive solution provides movement and mixing of the mass not only in two dimensions, however in a third essentially vertical dimension as well. Furthermore, the movements influenced to the mass are intermittent or periodical. Due to the severe improvement in tempering capacity of around 50%, around a third of the mass treatment chambers can be omitted in comparison with a traditional tempering apparatus having arms as stirring tools and if the same tempering capacity in kilos shall be available.

A thru 3-dimensional mixing pattern of the mass horizontally as well as vertically is achieved, when the all the obstacles at one side of an arm are projecting mixing blades, which are inclined so that the mass is forced radially out towards the periphery or radially in towards the centre. The frequency with which a specific area is swept by a revolving arm was then successfully increased with approximately 50% and the tempering capacity was even further improved.

The invention is further described by referral to the drawing, in which

figure 1 schematically and in vertical section discloses a tempering apparatus in which the mass treatment chambers are arranged in a column with intermediary heat exchange chambers for throughflowing liquid,

figure 2 discloses a schematical, vertical section of a mass treatment chamber comprising a mixing tool as in figure 1,

figure 3 discloses a perspective view of the mixing tool according to the invention disclosed in figure 2 with six arms,

figure 4 discloses a perspective view of a mixing tool with four arms, and

figure 5 discloses a perspective view of a further mixing tool with four arms.

The tempering apparatus 1 disclosed in figure 1 comprises a number of round or disc-shaped mass treatment chambers 2 and intermediary water chambers 3 arranged in a column. As depicted in a greater enlargement in figure 2 may each mass treatment chamber 2 be joined with an underlying water chamber 3 to a separate disc-shaped unit 4. The units 4 are then arranged on top of each other and joined to a column as depicted in figure 1, and the capacity of the apparatus 1 is determined simply by the number of units 4 in the column. Heat exchange between the mass chambers 2 and the neighbouring water chambers 3 takes place through the disc-shaped

walls

5 and 6, 7. The wall 7 may be omitted as the partitioning is then made by the wall 6 only being liquid-tight joined with the underlying unit 4 at the periphery and at the centre.

In each mass treatment chamber 2 is arranged a stirring tool 8, i.e. figure 2. The stirring tools 8 are all driven to rotation by a central shaft 9, which is driven by an electrical motor 10. The stirring tools are arranged vertically "floatable" on the shaft, so that they are able to move up and down a bit in the mass chamber, typically only 1-2 mm or less.

At the embodiment disclosed in figure 1 through-flow openings 11 for the mass to flow from one mass treatment chamber 2 and to the next chamber 2 in the column is arranged alternating at the periphery of the chambers 2. The through-flow openings may be arranged at other positions as well, and another typical position is as a ring-shaped opening extending around the shaft 9.

All of the water chambers 3 are connected to a water circuit, which for the sake of clarity is not disclosed as it doesn't perform part of the inventive idea. Water circuits is known in many configurations, however is that they are controllable, so that the desired tempering process can be performed up through the column, which the mass, and especially chocolate mass leaves having a content of stable β-crystals.

The stirring tools 8 comprise plate-shaped

arms

12, 13 as disclosed in figure 2 and 3. By the most preferred embodiment disclosed in figure 3, is arranged six arms of which three arms 12 are similar and three intermediary arms 13 are similar as well. The upper side 14 of the plate-shaped arms 12 comprises mixing obstacles in the form of projecting

mixing blades

15, 16, 17, 18, however the lower sides 19 are essentially free from mixing obstacles and thereby has a different geometrical configuration than the upper sides 14. The

knobs

20, 21 at the end of the

arms

12, 13 are not mixing obstacles as such but more serves to support the ends of the

arms

12, 13 against severe vertical movements in the chambers 2. Furthermore, the

knobs

20, 21 serves to take off the chocolate from the vertical, inner peripheral surface 22 of the mass chambers 2.

Each neighbouring plate-shaped arm 13 has the opposite geometrical configuration as that of the arms 12, so that the configuration of the upper side 23 of neighbouring arms 13 corresponds to the configuration of the lower side 19 of the arms 12, and the configuration of the lower side 24 of the arms 13 corresponds to the configuration of the upper side 14 of the arms 12. Arms having the configuration of the arm 12 is simply turned 180° or turned up-side down whereby the configuration of the arms 13 are obtained.

The mass is moved vertically up and down in the chamber in an intermittent sequence. The movements up and down of the mass works simultaneously with the radially forth and backwards mixing provided by the

mixing blades

15, 16, 17 and 18. The intermittent sequence of the vertically directed up- and downwardly directed flow of the mass highly effectively distributes the cold or heat from the heat exchange surfaces 26, 27 into the mass.

Tests have revealed an improvement of astonishing 30-60% in tempering capacity for the inventive solution in comparison with the traditional stirring tools with two or four plate-shaped arms. However, even more surprising were the results of comparative tests between the new stirring tools and a disc-shaped stirring tool of the previously described type. The capacity experienced by the new stirring tool disclosed in figure 3 was never lower than the capacity measured by the discs under the same conditions and by substitution of the tools in the same apparatus. The capacity was typically tested to be between 10 and 30% higher for the new stirring tool than for the known disc-shaped tool - and yet may the new apparatus be completely emptied from any mass and especially from highly viscous mass.

By different geometrical configuration is meant, that the shape of the one side 19 of an arm 12 secures a severely lower drag resistance or flow resistance through the mass, than the shape of the other side 14 of the arm 12. If mixing obstacles are provided on both sides of the arms the number of obstacles at the one side of the arm shall be much lesser than at the other side. At the one side may for example be arranged two obstacles and at the other side may be arranged 4-10 obstacles. The obstacles could for example be essentially identical mixing blades at both sides of the arm or identical mixing knobs at both sides of the arm. The drag resistance may also be reduces severely if the shape or configuration of the obstacles at the one side is altered, for example by reducing the width of the obstacles drastically in comparison with the width of the obstacles at the other side of the arms. Optional is when the one side is essentially free from mixing obstacles and the other side comprises 3- 6 mixing obstacles.

Decisive for obtaining different geometrical configuration of the two sides of the arms is then that a different resistance in the mass flow is achieved. When a pressure difference between the two sides is created, the mass is influenced to the intermittent up-and down movements behind the trailing edge of an arm. This movement or flow characteristic can easily be acknowledged by a 3D computer simulation or by a "live" test in which easily detected particles are observed in the mass chambers. The mass may be substituted by a transparent liquid with viscosity much like that of the mass to be tempered, such as chocolate mass. Parts of the test apparatus and the mass chambers is then transparent as well.

The rotation of the shaft 9 could also be raised in comparison with the stirring tools having only two arms. Apparently, the much better mixing in the inventive apparatus gives the possibility of a higher "sweeping" frequency of the arms over the heat exchange surfaces 26, 27 than by the prior known stirring tools with arms.

Close to the shaft may be arranged openings 25 in the

arms

12, 13 for through flow of the mass and for creating a better mixing of the mass close around the shaft 9. The

arms

12, 13 are arranged essentially in the middle between the upper heat exchange surfaces 26 and the lower surfaces 27, i.e. figure 2.

The embodiments of the

stirring tools

28 and 29 disclosed in figures 4 and 5 both comprises four plate-shaped arms. The

arms

30 and 31 of the stirring tool 28 are close to be identical to the

arms

12, 13 of the stirring tool 8 disclosed in figure 3. The only difference is, that the knobs 21 are omitted.

By the embodiment 29 disclosed in figure 5 the

arms

32 and 33 comprises mixing knobs 34. At the upper side 35 of the arms 32 and at the lower sides 36 of the arms 33 are arranged six mixing knobs 34 evenly distributed along the arms. At the other sides of the arms, i.e. the upper sides 37 of the arms 33 and the lower sides 38 of the arms 32, are arranged only two mixing knobs 34 so that the drag or flow resistance to the mass is severely reduced in comparison to the sides having a plurality of knobs. The intermittent up- and downwards movement of the mass is experienced and the improved capacity is obtained.

Claims

Apparatus for continuous tempering of fat-containing mass such as chocolat comprising
at least one mass treatment chamber (2) comprising a stirring tool (8) arranged therein and being driven by a central shaft (9),
which stirring tool (8) is free from a disc, as it only comprises mixing arms (12, 13), which are radially extending, plate shaped and having mixing obstacles (15, 16, 17, 18),
characterised in, that the upper side (14) of each plate shaped arm (12) has different geometrical configuration than the lower side (19) thereof, and that neighbouring plate-shaped arms (13) has the opposite configurations of the upper and the lower sides (23 and 24).
Apparatus according to claim 1, characterised in, that one side (14, 24) of each plate-shaped arm (12, 13) comprises mixing obstacles (15, 16, 17, 18), and the other side (19, 23) is free from mixing obstacles.
Apparatus according to claim 1, characterised in, that the plate-shaped arms (12, 13) are arranged essentially in the middle between upper and lower heat exchange surfaces (26, 27) of the mass treatment chamber (2).
Apparatus according to claim 1, characterised in, that the stirring tool (8) comprises four plate-shaped arms.
Apparatus according to claim 1, characterised in, that the stirring tool (8) comprises six plate-shaped arms.
Apparatus according to claim 1, characterised in, that the obstacles are projecting mixing blades (15, 16, 17, 18), which are inclined so that the mass is forced radially out towards the periphery or radially in towards the centre..